DK2237869T3 - Reactor for conducting high-pressure reactions, method of commissioning and method for conducting a reaction - Google Patents
Reactor for conducting high-pressure reactions, method of commissioning and method for conducting a reactionInfo
- Publication number
- DK2237869T3 DK2237869T3 DK09703667.7T DK09703667T DK2237869T3 DK 2237869 T3 DK2237869 T3 DK 2237869T3 DK 09703667 T DK09703667 T DK 09703667T DK 2237869 T3 DK2237869 T3 DK 2237869T3
- Authority
- DK
- Denmark
- Prior art keywords
- tube
- reactor
- conducting
- outer jacket
- nickel
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/06—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
- B01J8/067—Heating or cooling the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00539—Pressure
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00796—Details of the reactor or of the particulate material
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
The invention relates to a reactor for performing high-pressure reactions, comprising at least one tube (31) whose ends are each conducted through a tube plate (33) and which is bonded to the tube plate (33). The tube plates (33) and the at least one tube (31) are surrounded by an outer jacket, such that an outer space (39) is formed between the tube (31) and the outer jacket. The tube plates (33) each have at least one surface composed of a nickel-base alloy and the at least one tube (31) is in each case welded on to the surface composed of the nickel-base alloy. The surface composed of the nickel-base alloy points in each case in the direction of the particular reactor end. The outer jacket has a thickness which is sufficient to absorb tensile forces which occur between tube (31) and outer jacket owing to a temperature difference in the event of different expansion. The invention further relates to a process for starting up the reactor and for performing an exothermic reaction in the reactor.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP08150677 | 2008-01-25 | ||
EP08160471 | 2008-07-16 | ||
PCT/EP2009/050642 WO2009092724A1 (en) | 2008-01-25 | 2009-01-21 | Reactor for carrying out high pressure reactions, method for starting and method for carrying out a reaction |
Publications (1)
Publication Number | Publication Date |
---|---|
DK2237869T3 true DK2237869T3 (en) | 2011-12-05 |
Family
ID=40532542
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DK09703667.7T DK2237869T3 (en) | 2008-01-25 | 2009-01-21 | Reactor for conducting high-pressure reactions, method of commissioning and method for conducting a reaction |
Country Status (9)
Country | Link |
---|---|
US (1) | US20110009627A1 (en) |
EP (1) | EP2237869B1 (en) |
JP (1) | JP2011512241A (en) |
CN (1) | CN101977677B (en) |
AT (1) | ATE522271T1 (en) |
DK (1) | DK2237869T3 (en) |
RU (1) | RU2481887C2 (en) |
TW (1) | TW200948479A (en) |
WO (1) | WO2009092724A1 (en) |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8337757B2 (en) * | 2008-02-07 | 2012-12-25 | Precision Combustion, Inc. | Reactor control method |
JP2012512826A (en) | 2008-12-19 | 2012-06-07 | ビーエーエスエフ ソシエタス・ヨーロピア | Method for producing pure triethanolamine (TEOA) |
RU2592847C2 (en) | 2010-05-21 | 2016-07-27 | Басф Се | Method of producing 2-(2-tret.butylamino-ethoxy)-ethanol (tret.butylaminodiglycol, tbadg) |
US8455693B2 (en) | 2010-05-21 | 2013-06-04 | Basf Se | Process for preparing 2-(2-tert-butylaminoethoxy)ethanol (tert-butylaminodiglycol, TBADG) |
DE102014103691A1 (en) * | 2014-03-18 | 2015-09-24 | Basf Se | Heat exchanger, reactor assembly comprising this heat exchanger and method for controlling the temperature of a reactor |
JP2018500310A (en) | 2014-12-12 | 2018-01-11 | ビーエーエスエフ ソシエタス・ヨーロピアBasf Se | Method for producing polyetheramine |
EP3254026B1 (en) * | 2015-02-05 | 2018-09-26 | Casale Sa | Burner for the production of synthesis gas and related cooling circuit |
RU2649442C2 (en) * | 2016-04-25 | 2018-04-03 | Общество с ограниченной ответственностью "Старт-Катализатор" | Apparatus, method and catalyst for the purification of a gaseous raw hydrocarbon from hydrogen sulfide and mercaptans |
RU2649444C2 (en) * | 2016-04-25 | 2018-04-03 | Общество с ограниченной ответственностью "Старт-Катализатор" | Apparatus, method and catalyst for the drying and purification of a gaseous raw hydrocarbon from hydrogen sulfide and mercaptans |
CN111450778B (en) * | 2019-01-22 | 2023-04-07 | 中国石化工程建设有限公司 | Polymerization reaction system and method for preparing poly alpha-olefin |
WO2023135035A1 (en) | 2022-01-14 | 2023-07-20 | Basf Se | Method for the manufacture or conversion of alkanolamines |
WO2024073655A1 (en) * | 2022-09-29 | 2024-04-04 | Schneider Electric Systems Usa, Inc. | Direct electrical heating of process heater tubes using galvanic isolation techniques |
Family Cites Families (28)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1935053A (en) * | 1929-06-28 | 1933-11-14 | Selden Res & Engineering Corp | Catalytic apparatus |
US2618846A (en) * | 1947-08-15 | 1952-11-25 | Lummus Co | Method of plating tube sheets |
US3257710A (en) * | 1960-11-25 | 1966-06-28 | Westinghouse Electric Corp | Welded assembly and method of making such assembly |
US3257700A (en) * | 1965-02-08 | 1966-06-28 | E J Lavino & Co | Apparatus for manufacturing a refractory brick |
US3532472A (en) * | 1967-03-20 | 1970-10-06 | Shell Oil Co | Apparatus for carrying out partial oxidation of organic compounds |
CH493811A (en) * | 1967-09-06 | 1970-07-15 | Basf Ag | Heat exchange device |
US3617227A (en) * | 1969-05-05 | 1971-11-02 | Midland Ross Corp | Apparatus for catalytic reforming |
US3960700A (en) * | 1975-01-13 | 1976-06-01 | Cities Service Company | Coal hydrogenation to produce liquids |
US4221763A (en) * | 1978-08-29 | 1980-09-09 | Cities Service Company | Multi tube high pressure, high temperature reactor |
JPS6178738A (en) * | 1984-09-27 | 1986-04-22 | Mitsubishi Heavy Ind Ltd | Reactor |
JP2737914B2 (en) * | 1988-04-13 | 1998-04-08 | 三菱瓦斯化学株式会社 | Prussic acid reactor |
NL8902250A (en) * | 1989-09-08 | 1991-04-02 | Veg Gasinstituut Nv | METHOD FOR PERFORMING A CHEMICAL REACTION AND REACTOR TO BE USED THERE |
US5567398A (en) * | 1990-04-03 | 1996-10-22 | The Standard Oil Company | Endothermic reaction apparatus and method |
US6171570B1 (en) * | 1998-10-12 | 2001-01-09 | Kellogg Brown & Root, Inc. | Isothermal ammonia converter |
CN1320478A (en) * | 2000-04-24 | 2001-11-07 | 杭州林达化工技术工程有限公司 | Low-temp difference exothermic catalytic gas-solid phase reactor |
JP4092090B2 (en) * | 2001-06-26 | 2008-05-28 | 株式会社日本触媒 | Solid particle packed reactor and catalytic gas phase oxidation method using the reactor |
US7018591B2 (en) * | 2002-01-12 | 2006-03-28 | Saudi Basic Industries Corporation | High heat transfer tubular reactor |
DE10258180A1 (en) * | 2002-12-12 | 2004-06-24 | Basf Ag | Preparation of chlorine involves oxidation of hydrogen chloride and gas stream comprising molecular oxygen in presence of fixed-bed catalyst is carried out in reactor having annular and disk-shaped deflection plates between catalyst tubes |
DE10258153A1 (en) * | 2002-12-12 | 2004-06-24 | Basf Ag | Preparation of chlorine by gas-phase oxidation of hydrogen chloride by a gas stream having molecular oxygen in presence of a fixed-bed catalyst is carried out in reactor having bundle of parallel catalyst tubes and deflector plate |
CN100377773C (en) * | 2003-07-14 | 2008-04-02 | 三菱丽阳株式会社 | Fixed bed multitube reactor |
RU2259873C1 (en) * | 2004-03-22 | 2005-09-10 | Гордиенко Павел Сергеевич | Reactor |
RU2275332C2 (en) * | 2004-03-22 | 2006-04-27 | Павел Сергеевич Гордиенко | Reactor |
MY142153A (en) * | 2004-12-10 | 2010-09-30 | Shell Int Research | Reactor tube apparatus |
CN2841140Y (en) * | 2005-02-22 | 2006-11-29 | 浙江工业大学 | Nove cooling tube quenching type high-pressure methanol synthesizing internal component |
DE102005012209A1 (en) * | 2005-03-15 | 2006-09-28 | Basf Ag | Process for the preparation of an ethylamine |
DE102005047458A1 (en) * | 2005-09-30 | 2007-04-12 | Basf Ag | Preparation of aminodiglycol and morpholine, useful as solvent and stabilizer for synthesizing e.g. synthetic resins, comprises reacting diethyleneglycol with ammonia in the presence of a transition metal heterogeneous catalyst |
DE102005050284A1 (en) * | 2005-10-20 | 2007-05-10 | Basf Ag | Distributor device for a gas-liquid phase mixture for apparatus |
WO2008006749A1 (en) * | 2006-07-14 | 2008-01-17 | Basf Se | Method for producing an amine |
-
2009
- 2009-01-21 WO PCT/EP2009/050642 patent/WO2009092724A1/en active Application Filing
- 2009-01-21 DK DK09703667.7T patent/DK2237869T3/en active
- 2009-01-21 RU RU2010135156/05A patent/RU2481887C2/en not_active IP Right Cessation
- 2009-01-21 CN CN200980110401.XA patent/CN101977677B/en not_active Expired - Fee Related
- 2009-01-21 JP JP2010543482A patent/JP2011512241A/en active Pending
- 2009-01-21 EP EP09703667A patent/EP2237869B1/en not_active Not-in-force
- 2009-01-21 AT AT09703667T patent/ATE522271T1/en active
- 2009-01-21 US US12/864,540 patent/US20110009627A1/en not_active Abandoned
- 2009-01-22 TW TW098102680A patent/TW200948479A/en unknown
Also Published As
Publication number | Publication date |
---|---|
RU2010135156A (en) | 2012-02-27 |
EP2237869B1 (en) | 2011-08-31 |
RU2481887C2 (en) | 2013-05-20 |
TW200948479A (en) | 2009-12-01 |
US20110009627A1 (en) | 2011-01-13 |
CN101977677A (en) | 2011-02-16 |
WO2009092724A1 (en) | 2009-07-30 |
ATE522271T1 (en) | 2011-09-15 |
CN101977677B (en) | 2015-02-18 |
EP2237869A1 (en) | 2010-10-13 |
JP2011512241A (en) | 2011-04-21 |
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